Dynamic Intermediate-Temperature CO<sub>2</sub> Adsorption Performance of K<sub>2</sub>CO<sub>3</sub>-Promoted Layered Double Hydroxide-Derived Adsorbents

The dynamic adsorption characteristics of K<sub>2</sub>CO<sub>3</sub>-promoted layered double hydroxides (LDHs)-based adsorbent, with organic and inorganic anion intercalation, were studied. MgAl–LDH, K<sub>2</sub>CO<sub>3</sub>/MgAl–LDH, and K<sub&...

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Main Authors: Ruotong Li, Xixuan Hu, Liang Huang, Nicholas Mulei Musyoka, Tianshan Xue, Qiang Wang
Format: Article
Language:English
Published: MDPI AG 2024-03-01
Series:Molecules
Subjects:
Online Access:https://www.mdpi.com/1420-3049/29/6/1192
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author Ruotong Li
Xixuan Hu
Liang Huang
Nicholas Mulei Musyoka
Tianshan Xue
Qiang Wang
author_facet Ruotong Li
Xixuan Hu
Liang Huang
Nicholas Mulei Musyoka
Tianshan Xue
Qiang Wang
author_sort Ruotong Li
collection DOAJ
description The dynamic adsorption characteristics of K<sub>2</sub>CO<sub>3</sub>-promoted layered double hydroxides (LDHs)-based adsorbent, with organic and inorganic anion intercalation, were studied. MgAl–LDH, K<sub>2</sub>CO<sub>3</sub>/MgAl–LDH, and K<sub>2</sub>CO<sub>3</sub>/MgAl–LDH(C16) with varying K<sub>2</sub>CO<sub>3</sub> loads were prepared and used for intermediate-temperature CO<sub>2</sub> sequestration. The adsorbent was thoroughly characterized using X-ray diffraction, Brunauer–Emmett–Teller, scanning electron microscopy, and Fourier Transform Infrared Spectroscopy techniques, which revealed enhanced adsorption properties of MgAl–LDH, due to K<sub>2</sub>CO<sub>3</sub> promotion. Thermogravimetric CO<sub>2</sub> adsorption tests on the constructed adsorbent materials showed that the 12.5 wt% K<sub>2</sub>CO<sub>3</sub>/MgAl–LDH(C16) adsorbent with organic anion intercalation exhibited optimal adsorption activity, achieving an adsorption capacity of 1.12 mmol/g at 100% CO<sub>2</sub> and 350 °C. However, fixed-bed dynamic adsorption tests yielded different results; the 25 wt% K<sub>2</sub>CO<sub>3</sub>/MgAl–LDH prepared through inorganic anion intercalation exhibited the best adsorption performance in low-concentration CO<sub>2</sub> penetration tests. The recorded penetration time was 93.1 s, accompanied by an adsorption capacity of 0.722 mmol/g. This can be attributed to the faster adsorption kinetics exhibited by the 25 wt% K<sub>2</sub>CO<sub>3</sub>/MgAl–LDH adsorbent during the early stages of adsorption, thereby facilitating efficient CO<sub>2</sub> capture in low-concentration CO<sub>2</sub> streams. This is a conclusion that differs from previous reports. Earlier reports indicated that LDHs with organic anion intercalation exhibited higher CO<sub>2</sub> adsorption activity in thermogravimetric analyzer tests. However, this study found that for the fixed-bed dynamic adsorption process, K<sub>2</sub>CO<sub>3</sub>-modified inorganic anion-intercalated LDHs perform better, indicating their greater potential in practical applications.
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spelling doaj.art-75fa084ffb28411990ad71c1f926dd122024-03-27T13:56:42ZengMDPI AGMolecules1420-30492024-03-01296119210.3390/molecules29061192Dynamic Intermediate-Temperature CO<sub>2</sub> Adsorption Performance of K<sub>2</sub>CO<sub>3</sub>-Promoted Layered Double Hydroxide-Derived AdsorbentsRuotong Li0Xixuan Hu1Liang Huang2Nicholas Mulei Musyoka3Tianshan Xue4Qiang Wang5Engineering Research Center for Water Pollution Source Control & Eco-Remediation, College of Environmental Science and Engineering, Beijing Forestry University, Beijing 100083, ChinaEngineering Research Center for Water Pollution Source Control & Eco-Remediation, College of Environmental Science and Engineering, Beijing Forestry University, Beijing 100083, ChinaEngineering Research Center for Water Pollution Source Control & Eco-Remediation, College of Environmental Science and Engineering, Beijing Forestry University, Beijing 100083, ChinaNottingham Ningbo China Beacons of Excellence Research and Innovation Institute, University of Nottingham Ningbo China, Ningbo 315100, ChinaInstitute of Atmospheric Environment, Chinese Research Academy of Environmental Sciences, Beijing 100012, ChinaEngineering Research Center for Water Pollution Source Control & Eco-Remediation, College of Environmental Science and Engineering, Beijing Forestry University, Beijing 100083, ChinaThe dynamic adsorption characteristics of K<sub>2</sub>CO<sub>3</sub>-promoted layered double hydroxides (LDHs)-based adsorbent, with organic and inorganic anion intercalation, were studied. MgAl–LDH, K<sub>2</sub>CO<sub>3</sub>/MgAl–LDH, and K<sub>2</sub>CO<sub>3</sub>/MgAl–LDH(C16) with varying K<sub>2</sub>CO<sub>3</sub> loads were prepared and used for intermediate-temperature CO<sub>2</sub> sequestration. The adsorbent was thoroughly characterized using X-ray diffraction, Brunauer–Emmett–Teller, scanning electron microscopy, and Fourier Transform Infrared Spectroscopy techniques, which revealed enhanced adsorption properties of MgAl–LDH, due to K<sub>2</sub>CO<sub>3</sub> promotion. Thermogravimetric CO<sub>2</sub> adsorption tests on the constructed adsorbent materials showed that the 12.5 wt% K<sub>2</sub>CO<sub>3</sub>/MgAl–LDH(C16) adsorbent with organic anion intercalation exhibited optimal adsorption activity, achieving an adsorption capacity of 1.12 mmol/g at 100% CO<sub>2</sub> and 350 °C. However, fixed-bed dynamic adsorption tests yielded different results; the 25 wt% K<sub>2</sub>CO<sub>3</sub>/MgAl–LDH prepared through inorganic anion intercalation exhibited the best adsorption performance in low-concentration CO<sub>2</sub> penetration tests. The recorded penetration time was 93.1 s, accompanied by an adsorption capacity of 0.722 mmol/g. This can be attributed to the faster adsorption kinetics exhibited by the 25 wt% K<sub>2</sub>CO<sub>3</sub>/MgAl–LDH adsorbent during the early stages of adsorption, thereby facilitating efficient CO<sub>2</sub> capture in low-concentration CO<sub>2</sub> streams. This is a conclusion that differs from previous reports. Earlier reports indicated that LDHs with organic anion intercalation exhibited higher CO<sub>2</sub> adsorption activity in thermogravimetric analyzer tests. However, this study found that for the fixed-bed dynamic adsorption process, K<sub>2</sub>CO<sub>3</sub>-modified inorganic anion-intercalated LDHs perform better, indicating their greater potential in practical applications.https://www.mdpi.com/1420-3049/29/6/1192K<sub>2</sub>CO<sub>3</sub>-promoted LDHsorganic anion intercalationinorganic anion intercalationCO<sub>2</sub> dynamic adsorptionadsorption capacityintermediate-temperature
spellingShingle Ruotong Li
Xixuan Hu
Liang Huang
Nicholas Mulei Musyoka
Tianshan Xue
Qiang Wang
Dynamic Intermediate-Temperature CO<sub>2</sub> Adsorption Performance of K<sub>2</sub>CO<sub>3</sub>-Promoted Layered Double Hydroxide-Derived Adsorbents
Molecules
K<sub>2</sub>CO<sub>3</sub>-promoted LDHs
organic anion intercalation
inorganic anion intercalation
CO<sub>2</sub> dynamic adsorption
adsorption capacity
intermediate-temperature
title Dynamic Intermediate-Temperature CO<sub>2</sub> Adsorption Performance of K<sub>2</sub>CO<sub>3</sub>-Promoted Layered Double Hydroxide-Derived Adsorbents
title_full Dynamic Intermediate-Temperature CO<sub>2</sub> Adsorption Performance of K<sub>2</sub>CO<sub>3</sub>-Promoted Layered Double Hydroxide-Derived Adsorbents
title_fullStr Dynamic Intermediate-Temperature CO<sub>2</sub> Adsorption Performance of K<sub>2</sub>CO<sub>3</sub>-Promoted Layered Double Hydroxide-Derived Adsorbents
title_full_unstemmed Dynamic Intermediate-Temperature CO<sub>2</sub> Adsorption Performance of K<sub>2</sub>CO<sub>3</sub>-Promoted Layered Double Hydroxide-Derived Adsorbents
title_short Dynamic Intermediate-Temperature CO<sub>2</sub> Adsorption Performance of K<sub>2</sub>CO<sub>3</sub>-Promoted Layered Double Hydroxide-Derived Adsorbents
title_sort dynamic intermediate temperature co sub 2 sub adsorption performance of k sub 2 sub co sub 3 sub promoted layered double hydroxide derived adsorbents
topic K<sub>2</sub>CO<sub>3</sub>-promoted LDHs
organic anion intercalation
inorganic anion intercalation
CO<sub>2</sub> dynamic adsorption
adsorption capacity
intermediate-temperature
url https://www.mdpi.com/1420-3049/29/6/1192
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